Method of reclaiming a well completion brine solutions using an organic chelant
Abstract
A method of reclaiming a well completion brine solution by using an organic chelant that is capable of discriminating between (i) iron and/or non-zinc heavy metals; and (ii) calcium and zinc. The chelant is of the formula: and may be either a neutral compound, a corresponding salt, or a corresponding quaternary salt, wherein: D is F—A (Y 3 ) u (Y 4 ) v ; R is independently selected from C p or C p C(O); C p is a C 1 –C 36 hydrocarbyl group, optionally substituted with one or more substituents selected the group consisting of halogen, hydroxyl, sulfate, CH 2 CO 2 Z or —(CH 2 ) n PO(OZ) 2 groups; each A is independently selected from —N and —P; Y 1 is independently selected from J, —[(F)—A(J)] w Y 6 and R; J, R 1 , Y 2 , Y 3 , Y 4 , Y 5 and Y 6 are independently selected from the group consisting of —H, R, —(F) n CO 2 Z and —(CH 2 ) n PO(OZ) 2 ; each F is independently selected from a C 1 –C 12 hydrocarbyl group, optionally substituted with one or more substituents selected the group consisting of halogen, hydroxyl, sulfate, CH 2 CO 2 Z or —(CH 2 ) n PO(OZ) 2 groups; Z is —H or a balanced counterion of an alkali or alkaline earth metal or NH 4 + ; m is 0 to 7; n is 1 to 7; r+s+t is 1 or 2; u+v is 1 or 2; and w is 0 to 7 provided when m is 0, no more than one of R 1 , Y 1 , Y 2 and Y 5 can be —H.
Claims
exact text as granted — not AI-modified1. A method of reclaiming a well completion brine comprising the steps of:
(a.) mixing the brine containing metal impurities with a least one organic chelant for a time sufficient for the chelant to complex a metal and form a complexed metal precipitate, the organic chelant being a neutral compound or a corresponding salt of the formula:
wherein:
D is F—A(Y 3 ) n (Y 4 ) v ;
R is independently selected from C p or C p C(O);
C p is a C 1 –C 36 hydrocarbyl group, optionally substituted with one or more substituents selected the group consisting of halogen, hydroxyl, sulfate, CH 2 CO 2 Z or —(CH 2 ) n PO(OZ) 2 groups;
each A is independently selected from —N and —P;
Y 1 is independently selected from J, —[(F)—A(J)] w Y 6 and R;
J, R 1 , Y 2 , Y 3 , Y 4 , Y 5 and Y 6 are independently selected from the group consisting of —H, R, —(F) n CO 2 Z and —(CH 2 ) n PO(OZ) 2 ;
each F is independently selected from a C 1 –C 12 hydrocarbyl group, optionally substituted with one or more substituents selected the group consisting of halogen, hydroxyl, sulfate, CH 2 CO 2 Z or —(CH 2 ) n PO(OZ) 2 groups;
Z is —H or a balanced counterion of an alkali or alkaline earth metal or NH 4 + ;
m is 0 to 7;
n is 1 to 7;
r+s+t is 1 or 2;
u+v is 1 or 2; and
w is 0 to 7
provided when m is 0, no more than one of R 1 , Y 1 , Y 2 and Y 5 can be —H; and
(b.) removing the complexed metal precipitate from the brine
wherein the metal impurities contain iron and further wherein the complexed metal precipitate contains iron.
2. The method of claim 1 , wherein s and t are 0 and m is 1 to 7.
3. The method of claim 2 , wherein the at least one organic chelant is a compound or a corresponding salt of the formula:
wherein D represents random repeating blocks of F—A (Y 3 ) u (Y 4 ) v .
4. The method of claim 3 , wherein the at least one organic chelant is a compound of the formula:
wherein R 1 is —H, —(CH 2 ) n PO(OZ) 2 or —(F) n CO 2 Z; and Y 3 and Y 5 are independently selected from —(F) n CO 2 Z, —(CH 2 ) n PO(OZ) 2 and —H; and k is from 1 to 6.
5. The method of claim 4 , wherein k is 3.
6. The method of claim 5 , wherein at least one organic chelant is selected from the group consisting of:
(a.) R—N(CH 2 COOZ)—(CH 2 ) k —NH(CH 2 COOZ);
(b.) R—N(CH 2 COOZ)—(CH 2 ) k —N(CH 2 COOZ) 2 ;
(c.) R—NH—(CH 2 ) k —N(CH 2 COOZ) 2 ;
wherein R is C p or C p C(O).
7. The method of claim 6 , wherein the C p group is selected from C 8 to C 36 .
8. The method of claim 7 , wherein the C p group is selected from C 12 to C 36 .
9. The method of claim 8 , wherein the C p group is selected from C 12 to C 22 .
10. The method of claim 6 , wherein k is 3, Z is —H and R is a C 14 –C 22 hydrocarbyl group.
11. The method of claim 4 , wherein the at least one organic chelant is selected from the group consisting of:
(a.) R—N(CH 2 COOZ)—(CH 2 ) k —NH 2 ;
(b.) R—N(CH 2 COOZ)—(CH 2 ) k —NH(CH 2 COOZ)
(c.) R—NH—(CH 2 ) k —NH(CH 2 COOZ)
(d.) R—N(CH 2 COOZ)—(CH 2 ) k —N(CH 2 COOZ) 2 ;
(e.) R—NH—(CH 2 ) k —N(CH 2 COOZ) 2 ;
wherein R is C p or C p C(O).
12. The method of claim 11 , wherein k is 3.
13. The method of claim 11 , wherein k is 3, R is a C 14 –C 22 hydrocarbyl group and Z is —H.
14. The method of claim 3 , wherein at least one R 1 , Y 3 or Y 5 is —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 .
15. The method of claim 2 , wherein the at least one organic chelant is a compound of the formula:
wherein Y 3 is —H, C p or C p C(O), —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 ; and R 1 and Y 5 are independently selected from —(CH 2 ) n PO(OZ) 2 , —(F) n CO 2 Z and —H; and k is from 1 to 6.
16. The method of claim 15 , wherein k is 3.
17. The method of claim 15 , wherein the at least one organic chelant is selected from the group consisting of:
(a.) R—N (R 1 )—(CH 2 ) k —NH(CH 2 COOZ);
(b.) R—N (R 1 )—(CH 2 ) k —N(CH 2 COOZ) 2 ;
(c.) R—NH—(CH 2 ) k —NY 5 (CH 2 COOZ);
(d.) R—N(CH 2 COOZ)—(CH 2 ) k —NHY 5 ;
(e.) R—N(CH 2 COOZ)—(CH 2 ) k —NY 5 (CH 2 COOZ).
18. The method of claim 17 , wherein the at least one organic chelant is selected from the group consisting of R—NR 1 —(CH 2 ) k —N(CH 2 COOZ) 2 ; R—N(CH 2 COOZ)—(CH 2 ) k —N(CH 2 COOZ) 2 ; and R—N(CH 2 COOZ)—(CH 2 ) k —NY 5 (CH 2 COOZ).
19. The method of claim 17 , wherein each Z is —H.
20. The method of claim 17 , wherein R 1 is —(F) n CO 2 Z or —H.
21. The method of claim 2 , wherein the at least one organic chelant is a compound of the formula:
wherein Y 3 is —H, C p or C p C(O), —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 ; and R 1 and Y 5 are independently selected from —(F) n CO 2 Z, —(CH 2 ) n PO(OZ) 2 and —H; k is from 1 to 6; and at least one R 1 , Y 3 or Y 5 is —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 .
22. The method of claim 1 , wherein s, t and m are 0.
23. The method of claim 22 , wherein the at least one organic chelant is a compound of the formula:
wherein R 1 is —H, —(CH 2 ) n PO(OZ) 2 or —(F) n CO 2 Z; and Y 5 is —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 .
24. The method of claim 23 , wherein the at least one organic chelant is a compound of the formula:
R—NH(CH 2 COOZ) or R—N(CH 2 COOZ) 2 .
25. The method of claim 1 , wherein the at least one organic chelant is a salt and further wherein s is 0.
26. The method of claim 25 , wherein the salt is a compound of the formula:
wherein R 1 is —H, C p , —(CH 2 ) n PO(OZ) 2 or —(CH 2 ) n CO 2 Z; each of Y 4 and Y 5 are independently selected from —H, —(CH 2 ) n PO(OZ) 2 or —(CH 2 ) n CO 2 Z; X is an anion; and k and n are independently selected from 1 to 6.
27. The method of claim 1 , further comprising adding to the brine an absorbent, adsorbent or defoamer in an amount sufficient to reduce foaming.
28. The method of claim 1 wherein at least one J, R 1 , Y 2 , Y 3 , Y 4 , Y 5 or Y 6 is —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 .
29. A method of reclaiming a well completion brine comprising the steps of:
(a.) mixing the brine containing metal impurities with an organic chelant for a time sufficient for the chelant to complex a metal and form a complexed metal precipitate, wherein the organic chelant is at least one member selected from the group consisting of R—N (R 1 )—(CH 2 ) k —N(CH 2 COOZ) 2 ; R—N(CH 2 COOZ)—(CH 2 ) k —N(CH 2 COOZ) 2 ; and R—N(CH 2 COOZ)—(CH 2 ) k —NY 5 (CH 2 COOZ)
wherein
R is independently selected from C p or C p C(O);
C p is a C 12 –C 36 hydrocarbyl group, optionally substituted with one or more substituents selected from the group consisting of halogen, hydroxyl, sulfate, CH 2 CO 2 Z or —(CH 2 ) n PO(OZ) 2 groups;
R 1 and Y 5 are independently selected from —H, R, —(F) n CO 2 Z or —(CH 2 ) n PO(OZ) 2 ;
each F is independently selected from a C 1 –C 12 hydrocarbon group, optionally substituted with one or more substituents selected the group consisting of halogen, hydroxyl, sulfate, CH 2 CO 2 Z or —(CH 2 ) n PO(OZ) 2 groups;
Z is —H or a balanced counterion of an alkali or alkaline earth metal or NH 4 + ;
n is 1 to 7; and
k is from 1 to 6; and
(b.) removing the complexed metal precipitate from the brine wherein the metal impurities contain iron and further wherein the complexed metal precipitate contains iron.Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.